首页> 外国专利> process for the production of para xylene from the product of a paraselektiven disproportionierung of toluene by a kristallisierungsverfahren in connection with a adsorptionstufe in a simulated mobility bed

process for the production of para xylene from the product of a paraselektiven disproportionierung of toluene by a kristallisierungsverfahren in connection with a adsorptionstufe in a simulated mobility bed

机译:于模拟迁移率床中的吸附法,由kristallisierungsverfahren从甲苯的对位选择歧化产物中生产对二甲苯的方法

摘要

Prepn. of para-xylene from a toluene charge comprises: (a) a para-selective dismutation stage of toluene in the presence of H2 and a catalyst in a zone giving an effluent contg. benzene, toluene, xylenes enriched in para-xylene, ethylbenzene and aromatics of at least 9C; (b) a distillation stage of xylenes, separating benzene toluene and xylenes, in at least two columns; and (c) a high temp. crystallisation stage, pref. at +10 to -30 degrees C in at least one crystallisation zone producing para-xylene of a high purity and a mother liquor depleted in para-xylene. The mother liquor is contacted in an adsorption zone using a simulated mobile bed with a zeolite adsorbent in the presence of a desorbent (toluene) in conditions such as to give a prim. fraction (depleted in para-xylene and contg. toluene) and a secondary fraction enriched in para-xylene and contg. toluene. At least part of the secondary fraction is recycled to the crystallisation zone after having distilled off the toluene.
机译:准备来自甲苯进料的对二甲苯的步骤包括:(a)在存在H 2和催化剂的区域中,在产生废水的区域中,甲苯的对位选择性歧化阶段。苯,甲苯,对二甲苯,乙苯和芳烃含量至少为9C的二甲苯; (b)在至少两个塔中的二甲苯的蒸馏阶段,分离苯甲苯和二甲苯; (c)高温。结晶阶段在至少一个结晶区中,在+10至-30℃下产生高纯度的对二甲苯和母液中的对二甲苯贫化。在解吸剂(甲苯)的存在下,使用模拟移动床使母液在吸附区中与沸石吸附剂接触,以产生底漆。馏分(贫乏对二甲苯和续甲苯)和次级馏分富集对二甲苯和续甲苯。甲苯。蒸馏掉甲苯后,将至少部分二级馏分再循环到结晶区。

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